城市生活垃圾渗透系数测试研究

采用常水头测渗实验，对不同压实密度和水力梯度下的新鲜垃圾与陈垃圾的渗透系数进行测试，根据达西定律求得渗透系数值。由于垃圾的不均匀性、小颗粒的运动和大孔隙沟道流的形成和改变，实验初始阶段渗透系数值先增大至峰值，然后缓慢降低直至趋于稳定。实验稳定后，新鲜垃圾压实密度为0．75—0．95t／m^3时，渗透系数值约为1．26E-03～1．43E-03cm／s。陈垃圾在压实密度分别为1．2和1．4t／m^3时，渗透系数为8．29E-04和1．35E-04cm／s。     

厌氧陈腐垃圾模拟柱对渗滤液COD和NH_3-N的处理特性

通过实地钻取阿苏卫填埋场陈腐垃圾,真实模拟填埋场压实工艺,制作2种不同压实密度的陈腐垃圾模拟柱,对比研究其对渗滤液COD、NH3-N处理效果。结果表明,当模拟柱压实密度为1.09 t/m3时,渗滤液垂直运动明显;回灌此模拟柱水力负荷分别为18.6、28、37.2和46.5 L/t时,COD去除效果稳定,平均去除率达82...     

厌氧陈腐垃圾模拟柱对渗滤液COD和NH_3-N的处理特性

通过实地钻取阿苏卫填埋场陈腐垃圾,真实模拟填埋场压实工艺,制作2种不同压实密度的陈腐垃圾模拟柱,对比研究其对渗滤液COD、NH3-N处理效果。结果表明,当模拟柱压实密度为1.09 t/m3时,渗滤液垂直运动明显;回灌此模拟柱水力负荷分别为18.6、28、37.2和46.5 L/t时,COD去除效果稳定,平均去除率达82.4%,最高去除率可达90.1%;出水NH3-N浓度均值为549.3 mg/L,且介于415～700 mg/L间变化。自循环回灌COD去除率最高仅为11.5%,NH3-N去除率最高仅为11.8%,两者去除效果不明显。因此,北方平原型填埋场进一步完善填埋工艺,使填埋场垂直方向渗透系数分布均匀,充分利用陈腐垃圾堆体的自降解能力,才是处理渗滤液污染的关键。     

城市生活垃圾压缩站环境污染研究

通过对垃圾压缩站内生活垃圾进行采样分析、压实试验和环境污染检测，得出了城市生活垃圾压实密度和施加压力的关系曲线，确定了对垃圾压实的合适压力范围为0．1～0．2MPa；垃圾压缩站环境污染严重，垃圾压缩污水量为10-50kg／t，其中BOD5和COD平均分别超标111倍和486倍；环境噪音只有50m以外才能达到居民区环境质量二级标准（60dB（A））的噪音要求；产生的臭气在较低风速下一般扩散25m时污染达到最大，NH3、H2S分别可以达到0．011、0．0046mg／m^3，这个值占容许浓度的55％和46％。     

掺硼金刚石三电极系统处理垃圾渗滤液实验研究

实验以掺硼金刚石电极为阳极构建三电极系统处理稳定的垃圾渗滤液。考察了稀释比、初始pH值、电流密度和极板间距4个因素对垃圾渗滤液污染物去除率的影响。实验结果表明,电流密度、稀释比是影响电化学氧化垃圾渗滤液的主要因素,极板间距、初始pH值对电化学氧化垃圾渗滤液的影响较小。在稀释比为1∶2、电流密度为75 mA/cm2、pH值未调节、极板间距为10 mm最优工况时,经过5 h电化学氧化后NH+4-N、COD均能完全去除;NH+4-N、COD去除率分别满足线性方程y=21.759t、y=20.717t,对应的线性相关系数为0.9923和0.9925。最优工况条件下,BDD电极电化学氧化垃圾渗滤液的能耗为260 kWh/m3。     

菜场有机垃圾压缩脱水特性实验研究

为优化菜场垃圾压缩及脱水机械设计参数,获取最佳的压强值和垃圾在压缩仓内的保压时间,进行了菜场有机垃圾压缩脱水特性实验研究。通过压缩实验及对数据的分析,提出了有机垃圾压缩转运时的合理压缩强度范围为1.5～2.4 kg/cm2;通过压缩脱水实验及对数据的分析得到:压强一定时,保压时间越长,出水量越大;而保压时间一定时,压强增大,脱水率也增加,但2组数据变化均为非线性。对大白菜的实验表明,其合理的脱水压强和保压时间分别为2.4 kg/cm2和30 s左右。     

湍球塔和喷淋塔的海水脱硫冷态实验对比

通过湍球塔和喷淋塔的海水脱硫冷态实验对比,研究海水脱硫过程中烟气和海水参数对湍球塔和喷淋塔脱硫的不同影响。实验结果表明,SO2分压力增大,脱硫效率和尾水pH值减小;海水碱度、pH值和液气比增大,脱硫效率和尾水pH值也随之增大;湍球塔的脱硫效率和尾水pH值与液气比改变方式无关,实验用湍球塔的合适液气比值为2.3 L/m3;湍球塔脱硫实验中,塔内气速为1.58 m/s,SO2分压力为20 Pa,水温为10.2℃,液气比为1.1~2.8 L/m3时,尾水pH值在2.4~2.8之间;增大液气比时,喷淋塔改变海水流量的脱硫效果要比改变气体流量的脱硫效果明显;塔内气速1 m/s以上时,一级喷淋塔的脱硫效率要比湍球塔小很多,有时只有湍球塔的1/2左右。     

填料在净化污水过程中渗透性能变化趋势的研究

选取腐殖垃圾和砂以及两者质量比分别为4:1、3:2、2:3的混合物共5种填料,在1.0 m/d的水力负荷下,进行人工快速渗滤系统净化生活污水的试验,研究填料在进水过程中渗透性能的变化趋势.结果表明,腐殖垃圾的初始饱和水力渗透系数(K)最大,为3.32×10-2cm/s,而砂的初始K只有5.14×10-3cm/s,腐殖垃圾含量越大的混合物其仞始K也越大.在净化污水的过程中,5种填料的K逐渐减小,腐殖垃圾含量越大的混合物其K降幅也越大.随着进水时间的延长,各个填料柱填料层50～250 mm处的水头损失占总水头损失(填料层50～450mm处)的比例均逐渐增加,最终各个填料柱均发生堵塞,堵塞均发生在填料层50mm以上范围内.     

自来水厂污泥作填埋场覆盖材料的试验研究

作者对上海市闵行自来水厂污泥渗透系数、重金属含量、浸出液性质进行了分析研究 ,研究结果表明 ,在10 0kPa压力 (一般填埋场压实设备的压实压力 )下 ,污泥的渗透系数为 1.3× 10 -7cm/s ,符合国家规定 ,污泥可以作为填埋场终场覆盖材料。同时 ,边坡稳定的分析研究结果还表明 ,该厂污泥铺设的斜坡倾角不宜超过 16 .5度     

矿化垃圾基本理化性状剖面变化特征研究

矿化垃圾能否作为农业资源被重新利用,除应考虑有效植物营养物质的含量与是否存在有害物质外,还取决于其基本理化性状。对城市生活垃圾填埋场中经填埋6年、8年、10年后得到的矿化垃圾基本物化性状变化特征进行分析,结果表明:矿化垃圾的土粒密度显著小于对照土壤,交换性盐基总量、CEC显著大于对照土壤,pH值和对照土壤基本相当;表层(0~50 cm)矿化垃圾的土粒密度、CEC、交换性盐基总量、pH值的变化幅度依次大于中层(50~100 cm)和下层(100~150 cm);矿化垃圾的理化性状在填埋8~10年后总体趋于稳定。从植物生长的环境角度看,填埋8~10年后的矿化垃圾可以开采后作为植物生长基质、土壤改良剂等农业资源化利用。     

腐殖质含量对填料净化污水效能的影响

掺入与腐殖垃圾级配相同的砂配置腐殖质含量分别为1.09%、0.87%、0.65%、0.44%和0.01%的5种填料，装填0.5 m厚度的试验柱，构建人工快速渗滤系统处理生活污水，并测定饱和水力渗透系数，研究腐殖质含量对填料净化污水效能的影响。结果表明，在相同的水力负荷（1 m/d）和污染负荷下，5种腐殖质填料对COD和TP的平均去除率存在明显差异，腐殖质含量为1.09%、0.87%和0.65%的3种填料对COD的去除率较腐殖质含量为0.01%的填料均高出14%以上。腐殖质含量与TP去除率呈现正相关性。腐殖质含量最高的填料（1#）其初始K值最大达3.23×10^-2 cm/s，约为腐殖质含量最低的填料（5#）的5倍，其稳定运行时间最长。     

Comparison of the characteristics of flow-through and flow-around leaching tests of Solidified heavy metal wastes

This paper introduces a research work on studying the possibility of using a flow-through leaching test method to simulate the leaching behaviour of the cement-based stabilized/solidified (S/S) hazardous wastes. Both the flow-through leaching and the more common flow-around (dynamic leaching) test methods were carried out in the study to compare the leaching behaviour of the solidified waste under different leaching environments. The solidified waste samples were prepared from five kinds of heavy metals with two kinds of binders. The metals were Pb2+, Zn2+, Cu2+, Ni2+ (positive ions as nitrate), and Cr6+ (as a negative ion in potassium dichromate), and the binders were type I Ordinary Portland Cement (OPC) and Pulverised Fuel Ash (PFA). The results of two series of flow-through and flow-around leaching experiments are reported and compared in this paper. Mathematical models for simulating the leaching behaviour of the flow-through and flow-around leaching conditions were used to determine the diffusivities of the contaminants. The results show that, since the matrix of the solid waste in a flow-through leaching test is always being degraded, the diffusivities continuously increased during the leaching period. The range of the diffusivities was 10E-8 to 10E-3 cm2/s, which corresponds to the case of liquid phase diffusion. But in the case of the flow-around (dynamic leaching) test, the range of the diffusivities was 10E-18 to 10E-9 cm2/s which was similar to solid phase diffusion, and the variation of the diffusivity with time was not regular.     

厌氧折流板式微生物燃料电池堆影响因素研究

微生物燃料电池(MFC)中输出电压/电流的提升,以及反应器体积的扩展放大是其工程化应用的关键。本文构建了一个总体积为6.4 L的新型厌氧折流板式微生物燃料电池堆(ABSMFC)。以葡萄糖作为底物,探讨了阳极材料、液面高程差和水力停留时间(HRT)等因素对ABSMFC性能的影响。结果表明,碳纤维毡作为阳极时,电池单体外电路平均分压(R_(ex)=1 000Ω)为210 mV,填充石墨颗粒后增加到319.8 mV。格室间存在液面高程差时,电池单体、串联和并联的功率密度分别为207.1、181.1和215.7 mW/m~2,当无液面高程差(即水力相连)时为205.8、69.5和151.5 mW/m~2。4个电池单体串联和并联连接时,HRT对ABSMFC的产电稳定性无影响,溶解性COD的去除率和库仑效率均随HRT的增加而升高,且并联效果优于串联。     

Heterogeneity of chlorinated hydrocarbon sorption properties in a sandy aquifer

Hydraulic conductivity and sorption coefficients for chlorinated hydrocarbons (chloroform, carbon tetrachloride and tetrachloroethylene) were evaluated for 216 sediment samples collected across a 15 m transect and a 21 m depth interval in a contaminated aquifer near Schoolcraft, Michigan. Relationships between hydraulic conductivity, linear sorption partition coefficients, grain size classes, and spatial location were investigated using linear regression analysis and geostatistical techniques. Clear evidence of layering was found in sorption properties, hydraulic conductivity and grain sizes. Conductivity correlated well with grain size, as expected, but sorption varied inversely with grain size, contrary to some previous reports. No significant correlation was found between sorption properties and hydraulic conductivity. This is likely due to the unexpected presence of small amounts of highly sorptive coal-like solids, which dominate the sorption behavior but have little effect on conductivity. The results demonstrate that recent findings regarding the high sorption capacity of coal materials found in soils can exert a controlling influence on contaminant transport. Designers of in situ remediation systems should be cautioned that 1) it is not reasonable to assume that sorption capacity and hydraulic conductivity are related, 2) sorption capacity and hydraulic conductivity are critical measurements for contaminant site characterization and subsequent transport modeling, 3) estimating sorption capacity from organic carbon measurement may lead to greater errors than performing sorption isotherms, and 4) it is more important to characterize vertical heterogeneity rather than horizontal heterogeneity because both sorption and hydraulic conductivity are correlated across longer distances in the horizontal plane.     

利用废CRT屏玻璃为原料制备泡沫玻璃

以废阴极射线管(CRT)屏玻璃为主要原料,碳黑为起泡剂,采用粉末烧结法制备了低密度保温泡沫玻璃。通过扫描电镜(SEM)、导热系数测定仪等分析手段,研究了起泡剂的用量、发泡温度和发泡时间对泡沫玻璃泡径、密度、热学性能以及机械力学性能的影响。结果表明,在相同烧制工艺条件下,随起泡剂掺加量增加,烧制所得的泡沫玻璃密度成"V"型变化;当其掺加量为0.20%时,泡沫玻璃在密度、孔径分布以及力学性能上均达到最佳。随着发泡温度的提高和发泡时间的延长,密度会逐渐减小,泡沫玻璃的气泡会逐渐增大,以致产生连通现象。当发泡温度为820℃、发泡时间为30min时烧制的泡沫玻璃密度为0.180 g/cm3,导热系数为0.0695 W/(m.K)。     

生物转鼓过滤器反硝化净化NO的效率研究

采用自行研制的生物转鼓过滤器(RDB)反硝化净化NO。结果表明,在实验温度为25～30℃、pH为7.0～7.5、转鼓转速为1.0r/min、空床停留时间(EBRT)为86.40s、营养液用量为5.0L、营养液更换频率为0.2L/d的条件下,RDB在30d内完成挂膜;RDB稳定运行期间,当NO进气质量浓度为90～433mg/m3时,NO去除率维持在42.9%～85.2%,平均去除负荷为10.40g/(m3.h);转鼓转速决定了生物膜表面的更新速率和液膜厚度,当转速为0.5r/min时,NO去除率达到最大值(75.0%);将营养液用量控制在1.3～3.0L较为合理;EBRT是决定反硝化效率的重要因素,当EBRT为345.60s时,NO去除率不受其进气浓度的影响,且去除率高达95%以上,当EBRT为43.20s、NO进气质量浓度从98mg/m3增加到1095mg/m3时,NO去除率从62.5%下降到30.7%,当进气负荷为50.00g/(m3.h)时,NO去除负荷达到最大值(27.50g/(m3.h))。     

Effects of biofilm growth on flow and transport through a glass parallel plate fracture

The effects of biofilm growth on flow and solute transport through a sandblasted glass parallel plate fracture was investigated. The fracture was inoculated using soil microorganisms. Glucose, oxygen and other nutrients were supplied to support growth. The biomass initially formed discrete clusters attached to the glass surfaces, but over time formed a continuous biofilm. From dye tracer tests conducted during biofilm growth, it was observed that channels and low-permeability zones dominated transport. The hydraulic conductivity of the fracture showed a sigmoidal decrease with time. The hydraulic conductivity was reduced by a factor of 0.033, from 18 to 0.6 cm/s, corresponding to a 72% decrease in the hydraulic aperture, from 500 to 140 microm. In contrast, the mass balance aperture, determined from fluoride tracer tests, remained relatively constant, indicating that the impact of biomass growth on effective fracture porosity was much less than the effect on hydraulic conductivity. Analyses of pre-biofilm tracer tests revealed that both Taylor dispersion and macrodispersion were influencing transport. During biofilm growth, only macrodispersion was dominant. The macrodispersion coefficient alpha(macro) was found to increase logarithmically with hydraulic conductivity reduction.